US5595892A - Process for preparation of purified xanthan gum - Google Patents
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- US5595892A US5595892A US08/345,076 US34507694A US5595892A US 5595892 A US5595892 A US 5595892A US 34507694 A US34507694 A US 34507694A US 5595892 A US5595892 A US 5595892A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0024—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
- C08B37/0033—Xanthan, i.e. D-glucose, D-mannose and D-glucuronic acid units, saubstituted with acetate and pyruvate, with a main chain of (beta-1,4)-D-glucose units; Derivatives thereof
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
- C12P19/06—Xanthan, i.e. Xanthomonas-type heteropolysaccharides
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/8215—Microorganisms
- Y10S435/822—Microorganisms using bacteria or actinomycetales
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/8215—Microorganisms
- Y10S435/822—Microorganisms using bacteria or actinomycetales
- Y10S435/91—Xanthomonas
Definitions
- the present invention relates to a process for the preparation of purified xanthan gum. More particularly, it is directed to a process for the improvement of the transparency of a fermentation broth containing dissolved xanthan gum as well as aqueous solutions of xanthan gum by enzymatic treatment of the broth or aqueous solution.
- Xanthan gum can be obtained by conventional fermentation of a xanthan gum-producing bacterium, e.g., Xanthomonas campestris, a species in the genus Xanthomonas, and the like. It is recovered by precipitation with isopropanol from a fermented broth (This compound and process for preparing it are described in U.S. Pat. No. 3,659,026, column 4.)
- a xanthan gum-producing bacterium e.g., Xanthomonas campestris, a species in the genus Xanthomonas, and the like. It is recovered by precipitation with isopropanol from a fermented broth (This compound and process for preparing it are described in U.S. Pat. No. 3,659,026, column 4.)
- xanthan gum use, in place of Xanthomonas campestris, such other known xanthan gum-producing bacteria as Xanthomonas carotate, incanae, begoniae, papavericola, translucens, vasculorum, and hederae. All these species can produce a xanthan gum fermented broth.
- X50 and X59 are obtained by a selection procedure described in the above U.S. Patents, starting from publicly available strain NRRL 1459 which is referred to as X55.
- the broth at the end of fermentation of such strains contains from 0.5 to 2 percent by weight of undissolved matter including unconsumed nutrients and bacterial cell residues, in addition to about 2 to 5 percent by weight of xanthan gum.
- the aqueous solution of xanthan gum separated by extraction from the broth has low transparency. This presents problems in the fields where clear products are required, such as, the food and cosmetic industries, and in applications for secondary recovery of petroleum.
- European Patent Publication No. EP 78621, British Patent Application No. 8,132,564/1981 Japanese Patent Application No. 8,132,564/1981 (Japanese Patent Kokai No. 58-81792) teaches the use of acidic protease and neutral protease for this purpose.
- U.S. Pat. No. 4,119,491 Japanese Patent Kokoku No. 62-44918 teaches bringing a solution that results from protease treatment into contact with a siliceous solid matter and then removing the cellular debris from an aqueous polymer solution.
- U.S. Pat. No. 4,431,734 Japanese Patent Kokai No. 57-202303 proposes an enzymatic treatment using polysaccharase and protease.
- Patent Kokai No. 63-287494 teaches the combined use of a polygalacturonase active enzyme and a protease-active enzyme.
- European Patent Publication No. EP 39962 U.S. patent application Ser. No. 147812/1980 (Japanese Patent Kokai No. 57-5698) proposes the adoption of a composite enzyme having both ⁇ -1,3-glucanase- and protease-activities. None of the proposed treatments with protease have, however, proved satisfactorily effective.
- Japanese Patent No. 1318520 Japanese Patent Kokai No. 60-44919 introduces a treatment with the simultaneous addition of lysozyme, N-acetylmuramyl-L-alanine amidase, and peptidase. These enzymes are known to be able to lyse cell walls, but they have only slight action directly on Gram negative bacteria. Despite long treatment time required, their effect is disappointingly low.
- an object of the present invention is to provide a process for the preparation of xanthan gum having both excellent viscosity and transparency properties as measured by transmittance by the steps of first, heat-treating a fermentation broth containing xanthan gum or an aqueous solution of xanthan gum under specific pH and temperature conditions, thereafter treating the broth sequentially with alkaline protease and with lysozyme or vice versa, and thereafter separating solid xanthan gum by extraction from the treated broth using an organic solvent, e.g., isopropyl alcohol.
- An aqueous solution of 0.3 percent by weight of the solid xanthan gum thus obtained has a transparency (transmittance)of at least 80 percent as measured by the methods described herein.
- xanthan gum is prepared by subject strain X50 or X59 to fermentation conditions to produce a fermentation broth containing xanthan gum, and cellular and bacterial debris. The broth thus obtained is then subjected to the above described sequential heat treatment and enzymes steps.
- xanthan gum which exhibits a transmittance of at least 75% by weight in 1.0% aqueous solution, and, preferably, at least 80% in 1.0% by weight aqueous solution.
- xanthan gum having a transmittance of at least 90% in 0.3% by weight aqueous solution can be obtained.
- transmittance means the transmittance of an aqueous solution of the indicated weight percent xanthan at a wavelength of 650 nm and measured as described hereinafter.
- the invention thus provides a process for preparing highly transparent fermented xanthan gum by a heat treatment at an initial pH of at least 9 and an immediately ensuing enzymatic treatment with alkaline protease and then lysozyme (or vice versa) thoroughly the solubilize water insoluble bacterial cell residues and culture medium-derived undissolved matter, without adversely affecting the viscosity properties characteristic of xanthan gum.
- the heat treatment can be performed at an initial pH of from 9 to 12.5, preferably from 10 to 12, and at a temperature of from 45° to 70° C., preferably from 50° to 60° C., for at least 30 minutes. If the pH is below 9, the bacterial solubilization sometimes does not proceed efficiently, leading to unfavorable results. If it is above 12.5 the broth could be colored or the viscosity properties of the product impaired. Although the pH naturally decreases during the course of the treatment, it should preferably be maintained above 8. Any temperature below 45° C. is undesirable because it may hamper efficient solubilization of bacteria in the enzymatic treatment.
- a temperature above 70° C. is again undesirable because it can cause coloring of the broth or adverse effects upon the viscosity properties of the product.
- Treatment for no less than 30 minutes gives a sufficient effect, but a treatment time of more than 2 hours is not advisable since it can decrease the productivity.
- the heat treatment must precede the enzymatic treatment. Without this pretreatment, the enzymatic treatment would not be effective or take a prolonged time period before it proves effective.
- Example 5 hereof it is possible to achieve good results at heating temperature up to 80° C. and an initial pH as low as 7.
- the enzymatic treatment is carried out in two steps using alkaline protease and lysozyme.
- the duration of each treatment step is desirably between 20 minutes and 5 hours. A period shorter than 20 minutes is not desirable in that the treatment effect is not fully achieved. Treatment for more than 5 hours would not bring any additional treatment effect, leading to reduced productivity.
- Treatment with alkaline protease is conducted at a pH in the range from 6.0 to 10.0, preferably from 7.5 to 9.0, at a concentration of 10 to 500 ppm, and at a temperature of 40° to 65° C. for at least 20 minutes.
- a temperature below 40° C. is not recommended from the viewpoint of productivity because lowered enzymatic activity would call for a treating time of more than 6 hours.
- a temperature above 65° C. would deactivate the enzyme, making the treatment non-effective.
- Acidity below 9 of pH 6.0 would deactivate alkaline protease, while a pH above 10.0 is also undesirable since it can deteriorate the physical properties of the product. If the concentration is below 10 ppm, a satisfactory effect would not result despite extension of the treating time. Conversely a concentration in excess of 500 ppm is not advisable because of higher production costs; an excessive concentration does not produce any further improvements.
- Treatment with lysozyme is done at a pH value in the range of 5.5 to 8.0, preferably between 6.5 and 7.5, a concentration of 0.5 to 100 ppm, and a temperature of 25° to 45° C. and even up to 60° C. for at least 20 minutes.
- a temperature above 60° C. is undesirable because it can lower the activity of lysozyme in some cases.
- lysozyme would not be active and, below 5.5 the physical properties of the product could deteriorate. If the concentration is less than 0.5 ppm prolonged treatment would become necessary, and even if treatment time is prolonged it may not lead to any meaningful effects.
- a concentration of more than 100 ppm is not warranted from an economical standpoint. Any of the two enzymatic treatment steps may precede the other.
- Enzymes useful for the reduction of the invention to practice are: an alkaline protease produced by a bacterium in the genus Bacillus, such as, B. subtilis, and a lysozyme known as endo- ⁇ -1,4-N-acetylhexosaminidase which hydrolyzes the ⁇ -1,4 bonds of N-acetylglucosamine and N-acetylmuramic acid in bacterial cell walls.
- alkaline proteases produced by B. licheniformis, B. amylaliquifaciens, and B. pumilis are known besides that which originates from B. subtilis.
- lysozymes there are known animal lysozymes, such as, egg white lysozymes of chickens, ducks, quails, turkeys, and geese, spleen lysozymes of dogs and rats, and lysozymes present in human urine (of leukemia patients), human milk, and tears. Plant lysozymes have been found in turnips, cabbages, and papaya juice. For the present invention, however, the origins of the enzymes are of little importance.
- the process according to the invention permits the omission of such complex process steps as dilution, cake filtration, and concentration that have hitherto been required for the removal of undissolved matter. This brings ease of operation and economical advantage. A further advantage is high transparency of the product that ordinary enzymatic processes have failed to realize.
- An important aspect of the present invention is our discovery that when specific hyperproducing X. campestris are used to generate the xanthan gum, the clarification process of the present invention yields a xanthan gum product exhibiting substantially improved transparency compared to the parent X. campestris strain from which they are derived.
- Strain X59 which is a rifampicin resistant strain
- strain X50 which is a rifampicin and bacitracin resistant strain of X. campestris are considered hyperproducers to the extent that the strains exhibit enhanced productivity of xanthan gum as compared to strain X55 from which the hyperproducing strains are derived by a selection process as described in U.S. Pat. 5,194,386 and application Ser. No.
- inventive clarification process may be carried out on the fermentation broth, i.e., the broth after completion of the fermentation process, or, alternatively, on recovered xanthan product (i.e., in water).
- a medium of composition II was placed in a 30-liter fermenter and inoculated with a Xanthomonas campestris broth of X59 that had been cultured for 24 hours on a medium of composition I. It was then cultured under aeration and agitation at pH 6.5 to 7.0 and at 30° C. for two days, and a broth containing 30 g xanthan gum per liter was obtained. With stirring the broth was heat-treated at an initial pH of 11° and at 55° C. for 90 minutes and, while being kept at 55° C.
- the broth was adjusted to pH 8.5 and, after the addition of 300 ppm alkaline protease ("Bioplase", a product of Nagase Biochemical Co.), the mixture was treated with stirring at 55° C. for two hours. Next, the resulting broth was cooled down to 35° C., 3 ppm lysozyme ("Lysozyme Taiyo", a product of Taiyo Chemical Co.) was added, and the mixture was further treated with stirring at 35° C. for one hour.
- a broth prepared in the same way as described in Example 1 was enzymatically treated in the reverse order. After cooling, it was adjusted to pH 7.0 and, with the addition of 3 ppm lysozyme ("Lysozyme Taiyo" of Taiyo Chemical), the mixture was treated with stirring at 35° C. for two hours. Next, the broth was heated to 55° C., 300 ppm alkaline protease ("Bioplase” of Nagase Biochemical) was added, and the mixture was treated with stirring at 55° C. for one hour.
- the broth was sampled after each of the process steps, i.e., after the conclusion of fermentation, the heat treatment, and the first and second stages of enzymatic treatment.
- Xanthan gum was separated by extraction from the test broth using 1.6 times by weight of isopropyl alcohol, and the extract was air dried.
- An aqueous solution containing 0.3 percent by weight of the thus obtained solid xanthan gum was prepared, and the sample was tested for light transmittance and viscosity (with a Brookfield viscometer at 30 rpm). Table 1 summarizes the results.
- Example 2 The procedure of Example 1 was repeated for treatments except that the lysozyme concentration was varied. The results are given in Table 2.
- Fermentation performed in the same manner as in Example 1 yielded a broth containing 30 g xanthan gum per liter.
- the broth at an initial pH of 7.0 was heat treated at 80° C. for 90 minutes and then cooled to and kept at 55° C. After the cooling the pH was adjusted to 8.5, and 300 ppm alkaline protease ("Bioplase” of Nagase Biochemical) was added, and the mixture was treated with stirring at 55° C. for two hours.
- the broth was cooled down to 35° C. and after the addition of 3 ppm lysozyme ("Lysozyme Taiyo" of Taiyo Chemical), the mixture was treated with stirring at 35° C. for one hour.
- the broth was sampled after each of the process steps, i.e., after the conclusion of fermentation, the heat treatment, and the first and second stages of enzymatic treatment.
- Xanthan gum was separated by extraction from the test broth using 1.6 times by weight of isopropyl alcohol, and the extract was air dried.
- An aqueous solution containing 0.3 percent by weight of the thus obtained solid xanthan gum was prepared, and the sample was tested for light transmittance and viscosity (with a Brookfield viscometer at 30 rpm). Table 3 shows the results.
- the invention procedure enables the production of xanthan gum having excellent viscosity, e.g., at least greater than about 175 cp (0.3% by weight solution with Brookfield viscometer at 30 rpm).
- Fermentation and heat treatment were carried out in a manner similar to Example 1, and either lysozyme or alkaline protease alone was used in enzymatic treatment.
- the conditions for treatment with either enzyme were the same as used in Example 1.
- xanthan gum was separated from the resulting broth by extraction with 1.6 times by weight of isopropyl alcohol and the extract was air dried.
- An aqueous solution containing 0.3 percent by weight of the xanthan gum so obtained was prepared and tested for light transmittance and viscosity. As Table 4 indicates, the solutions thus prepared failed to attain, despite extended treating periods, the high transparency that the process of the present invention achieves.
- Example 2 In the manner described in Example 1, fermentation and heat treatment were performed, with the exception that the enzymatic treatment used lysozyme and alkaline protease together.
- the reaction conditions were pH 7.5 and 45° C. at which both enzymes were active.
- 300 ppm Bioplase and 3 ppm lysozyme the reaction was carried out for 6 hours. After each treating time the sample was tested for light transmittance and viscosity as was the case with Comparative Example 1. The results are given in Table 5.
- Example 1 The fermentation of Example 1 was directly by the two stage enzymatic treatment without the heat treatment. Samples of the individual process steps were tested for light transmittance and viscosity. Table 6, which shows the results, indicates that the omission of heat treatment reduced the enzymatic effects of the resulting broths.
- xanthan gum was produced by the submerged fermentation of strains X59 and X50.
- the fermentation procedures were carried out using conventional aerobic submerged fermentation techniques normally used for fermentation of X. campestris.
- the fermenter size was a 5 liter jar for these experiments.
- the broths from each of the terminated fermentations were adjusted to pH 11 and then heated at 55° C. for 90 minutes. Thereafter, a series of four 200 ml aliquots from each of the resulting broths were treated as follows:
- Each of the four aliquots were treated with a different system of protease and lysozyme enzymes.
- the pH of the aliquot was adjusted to an appropriate pH for the particular protease.
- Table 7 sets forth a series of proteases commercially available and their optimum pHs and temperatures of use. Also shown is a Food Grade Lysozyme which was used in addition to the Lysozyme Taiyo used in the previous experiments.
- the details of the fermentation, the final amount of xanthan gum obtained, the final cellular and the ratio of cellular debris to xanthan gum are shown in Table 8.
- the optical density of a 1 to 7 dilution of the initial broth, the solution obtained after the heat treatment, the solution obtained after the protease treatment, and the solution obtained after the lysozyme treatment, as well as the transmittance of a 1 wt. % solution of precipitated xanthan product obtained after the heat and enzyme treatments are shown in Table 9.
- the particular enzymes, temperatures and pH of the treatments used are detailed after Table 9.
- the transmittance was measured using a quartz cell having a cell length of 2 cm with a lightwave length of 650 nm. Measurements were made with a photoelectric colorimeter 5E-type available from Kotaki Trading. The optical density at 660 nm was measured using a cell having a cell length of 1 cm and a dilution of 7 times by weight. Measurements were made with a UV visible recording spectrophotometer UV-160 type available from Shimazu. The results of these experiments show that substantially higher clarification of broths obtained from the fermentation of X59 are obtained by the inventive treatments as compared to the broth obtained from the fermentation of X55.
- the powder is mixed with water resulting in dissolution of the enzyme into the aqueous phase.
- the calcium carbonate is separated from the aqueous phase and it is the aqueous phase which is used.
- concentrations of enzymes are indicated as the concentration in the solution to which they are added, e.g., 500 ppm of enzymes means that in the aliquot or broth, the concentration of enzyme in solution for the treatment was 500 ppm.
- Strain X55 was used. A production media was placed in a 30 liter fermenter and inoculated with a Xanthornonas campestris broth that had been cultured for 24 hours in seed media. It was then cultured under aeration and agitation at pH 6.5 to 7.0 and at 30° C. for two days, and a broth containing 20 g xanthan gum per liter was obtained. The broth was heat-treated with stirring at an initial pH of 11 and at 55° C. for 90 minutes and while being kept at 55° C., the broth was adjusted to pH 8.5 with 10% aqueous H 2 SO 4 .
- Example 1 The procedure of Example 1 was repeated except that protease Multifect P-64, a product of Genencor, was used in place of Bioplase and lysozyme "Canadian Lysozyme", a product of Food Grade Lysozyme, was used in place of Lysozyme Taiyo.
- Example 1 The procedure of Example 1 was repeated except that strain X59 was used in place of X55.
- Example 1 The procedure of Example 1 was repeated except that strain X59 was used in place of X55, protease "Multifect P-64" was used in place of Bioplase and lysozyme "Canadian Lysozyme” was used in place of Lysozyme Taiyo.
- Example 1 The procedure of Example 1 was repeated except that strain X50 was used in place of X55.
- Example 1 The procedure of Example 1 was repeated except that strain X59 was used in place of X55 and Media 2 was used in place of Media 1.
- Example 1 The procedure of Example 1 was repeated except that strain X50 was used in place of X55 and that Media 2 was used in place of Media 1.
- a broth was prepared used in strain X59 in place of X55 in the same way as described in Example 1.
- the resulting broth was enzymatically treated in the reverse order, that is, after heat-treatment, it was adjusted to pH 6.5 and, after the addition of aqueous solution of 0.054 g (3 ppm) lysozyme, "Lysozyme Taiyo", the mixture was heated with stirring at 55° C. for one hour.
- a supernatant of aqueous solution of 9.0 g (500 ppm) alkaline protease "Bioplase” was added and the mixture was heated with stirring at 55° C. for two hours.
- Lysozyme Treatment 3 ppm, pH 6.5, 55° C., 60 minutes ("Lysozyme Taiyo", a product of Taiyo Chemical Co.)
- Lysozyme treatment 30 ppm, pH 6.5, 55° C., 60 minutes ("Canadian Lysozyme", a product of Food Grade Lysozyme).
- broths and xanthan gum produced from strains X59 and X50 exhibit substantially superior transmittance using the inventive procedure as compared to the original strain X55.
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Abstract
The process includes heat-treating a xanthan gum fermented broth, and consecutively treating the broth first with alkaline protease and then with lysozyme or in reverse order, and thereafter recovering xanthan gum from the treated broth. A clear aqueous solution of xanthan gum may be obtained Without complex procedures.
Description
This application is a continuation-in-part of application Ser. No. 07/990,758, filed Dec. 15, 1992, the contents of which are hereby incorporated by reference.
1. Field of the Invention
The present invention relates to a process for the preparation of purified xanthan gum. More particularly, it is directed to a process for the improvement of the transparency of a fermentation broth containing dissolved xanthan gum as well as aqueous solutions of xanthan gum by enzymatic treatment of the broth or aqueous solution.
2. Description of the Related Art
Xanthan gum can be obtained by conventional fermentation of a xanthan gum-producing bacterium, e.g., Xanthomonas campestris, a species in the genus Xanthomonas, and the like. It is recovered by precipitation with isopropanol from a fermented broth (This compound and process for preparing it are described in U.S. Pat. No. 3,659,026, column 4.)
Other processes for the manufacture of xanthan gum use, in place of Xanthomonas campestris, such other known xanthan gum-producing bacteria as Xanthomonas carotate, incanae, begoniae, papavericola, translucens, vasculorum, and hederae. All these species can produce a xanthan gum fermented broth.
U.S. Pat. Nos. 5,310,677, 5,194,386 and U.S. patent application Ser. No. 07/826,095, filed Jan. 27, 1992, the contents of each of which are incorporated herein by reference, discloses several hyperproducing strains of X. campestris and methods for obtaining these strains. In particular, two strains identified as X50 (ATCC 55429) and X59 (ATCC 55298), each of which is available from the American Type Culture Collection pursuant to Budapest Treaty, have been deposited on Feb. 18, 1992, with the American Type Culture Collection in Rockville, Md., and all restrictions of the availability to the public of the materials so deposited will be irrevocably removed upon the granting of a patent thereon. X50 and X59 are obtained by a selection procedure described in the above U.S. Patents, starting from publicly available strain NRRL 1459 which is referred to as X55. The broth at the end of fermentation of such strains contains from 0.5 to 2 percent by weight of undissolved matter including unconsumed nutrients and bacterial cell residues, in addition to about 2 to 5 percent by weight of xanthan gum. The aqueous solution of xanthan gum separated by extraction from the broth has low transparency. This presents problems in the fields where clear products are required, such as, the food and cosmetic industries, and in applications for secondary recovery of petroleum.
Known methods for the purification and clarification of xanthan gum, and solutions and fermentation broths thereof depend on centrifugation or cake filtration for the removal of the undissolved matter from the broth. In either case, however, the broth as obtained from the fermentation is so viscous that it must be diluted with water which adds to the cost and complexity of the process and makes such methods impractical. A variation of those methods suggests heating of the broth to enhance its filtration properties.
One effective approach is solubilizing the undissolved matter in the broth by enzymatic treatment. Many proposals have hitherto been made in this direction.
For example, (Japanese Patent Provisional Publication (Kokai) No. 50-121493) and U.S. Pat. Nos. 3,966,618/1976, 4,010,071/1977, and 4,165,257/1979 propose clarification by use of alkaline protease and neutral protease. They report, in fact, that xanthan gum solutions cannot necessarily be made absolutely clear or transparent and the solutions retain some degree of turbidity.
European Patent Publication No. EP 78621, British Patent Application No. 8,132,564/1981 (Japanese Patent Kokai No. 58-81792) teaches the use of acidic protease and neutral protease for this purpose. U.S. Pat. No. 4,119,491 (Japanese Patent Kokoku No. 62-44918) teaches bringing a solution that results from protease treatment into contact with a siliceous solid matter and then removing the cellular debris from an aqueous polymer solution. U.S. Pat. No. 4,431,734 (Japanese Patent Kokai No. 57-202303) proposes an enzymatic treatment using polysaccharase and protease. U.S. Pat. 4,904,586 (Japanese Patent Kokai No. 63-287494) teaches the combined use of a polygalacturonase active enzyme and a protease-active enzyme. European Patent Publication No. EP 39962, U.S. patent application Ser. No. 147812/1980 (Japanese Patent Kokai No. 57-5698) proposes the adoption of a composite enzyme having both β-1,3-glucanase- and protease-activities. None of the proposed treatments with protease have, however, proved satisfactorily effective.
Among other enzymatic processes so far proposed are the utilization of a nuclease-active enzyme according to U.S. Pat. No. 4,729,958 (Japanese Patent Kokai No. 61-146193) and the purification by the action of cellulase according to U.S. Pat. No. 4,416,990 (Japanese Patent Kokai No. 57-91194). These processes also have failed to be adequately effective.
Japanese Patent No. 1318520 (Japanese Patent Kokai No. 60-44919) introduces a treatment with the simultaneous addition of lysozyme, N-acetylmuramyl-L-alanine amidase, and peptidase. These enzymes are known to be able to lyse cell walls, but they have only slight action directly on Gram negative bacteria. Despite long treatment time required, their effect is disappointingly low.
Thus, the known methods for removing water-insoluble microbial residues and culture medium-derived undissolved matter, including the methods relying upon centrifugation or cake filtration or upon enzymatic treatment to make the undissolved matter soluble in water, have not produced a satisfactory xanthan gum or solution thereof with the desired high degree of transparency.
We have discovered a new and superior method for the clarification of a xanthan gum fermented broth and aqueous solution of xanthan gum. In addition, we have discovered that particularly superior product transparency can be obtained by using X50 and X59 as the gum producing strains.
Thus, an object of the present invention is to provide a process for the preparation of xanthan gum having both excellent viscosity and transparency properties as measured by transmittance by the steps of first, heat-treating a fermentation broth containing xanthan gum or an aqueous solution of xanthan gum under specific pH and temperature conditions, thereafter treating the broth sequentially with alkaline protease and with lysozyme or vice versa, and thereafter separating solid xanthan gum by extraction from the treated broth using an organic solvent, e.g., isopropyl alcohol. An aqueous solution of 0.3 percent by weight of the solid xanthan gum thus obtained has a transparency (transmittance)of at least 80 percent as measured by the methods described herein.
In another embodiment of the invention, xanthan gum is prepared by subject strain X50 or X59 to fermentation conditions to produce a fermentation broth containing xanthan gum, and cellular and bacterial debris. The broth thus obtained is then subjected to the above described sequential heat treatment and enzymes steps. With this embodiment, it is possible to obtain xanthan gum which exhibits a transmittance of at least 75% by weight in 1.0% aqueous solution, and, preferably, at least 80% in 1.0% by weight aqueous solution. In addition, with the present invention, xanthan gum having a transmittance of at least 90% in 0.3% by weight aqueous solution can be obtained. As used herein, transmittance means the transmittance of an aqueous solution of the indicated weight percent xanthan at a wavelength of 650 nm and measured as described hereinafter.
More specifically, the invention thus provides a process for preparing highly transparent fermented xanthan gum by a heat treatment at an initial pH of at least 9 and an immediately ensuing enzymatic treatment with alkaline protease and then lysozyme (or vice versa) thoroughly the solubilize water insoluble bacterial cell residues and culture medium-derived undissolved matter, without adversely affecting the viscosity properties characteristic of xanthan gum.
The heat treatment can be performed at an initial pH of from 9 to 12.5, preferably from 10 to 12, and at a temperature of from 45° to 70° C., preferably from 50° to 60° C., for at least 30 minutes. If the pH is below 9, the bacterial solubilization sometimes does not proceed efficiently, leading to unfavorable results. If it is above 12.5 the broth could be colored or the viscosity properties of the product impaired. Although the pH naturally decreases during the course of the treatment, it should preferably be maintained above 8. Any temperature below 45° C. is undesirable because it may hamper efficient solubilization of bacteria in the enzymatic treatment.
A temperature above 70° C. is again undesirable because it can cause coloring of the broth or adverse effects upon the viscosity properties of the product. Treatment for no less than 30 minutes gives a sufficient effect, but a treatment time of more than 2 hours is not advisable since it can decrease the productivity. The heat treatment must precede the enzymatic treatment. Without this pretreatment, the enzymatic treatment would not be effective or take a prolonged time period before it proves effective. However, as shown in Example 5 hereof it is possible to achieve good results at heating temperature up to 80° C. and an initial pH as low as 7.
The enzymatic treatment is carried out in two steps using alkaline protease and lysozyme. The duration of each treatment step is desirably between 20 minutes and 5 hours. A period shorter than 20 minutes is not desirable in that the treatment effect is not fully achieved. Treatment for more than 5 hours would not bring any additional treatment effect, leading to reduced productivity.
Treatment with alkaline protease is conducted at a pH in the range from 6.0 to 10.0, preferably from 7.5 to 9.0, at a concentration of 10 to 500 ppm, and at a temperature of 40° to 65° C. for at least 20 minutes. A temperature below 40° C. is not recommended from the viewpoint of productivity because lowered enzymatic activity would call for a treating time of more than 6 hours. A temperature above 65° C. would deactivate the enzyme, making the treatment non-effective. Acidity below 9 of pH 6.0 would deactivate alkaline protease, while a pH above 10.0 is also undesirable since it can deteriorate the physical properties of the product. If the concentration is below 10 ppm, a satisfactory effect would not result despite extension of the treating time. Conversely a concentration in excess of 500 ppm is not advisable because of higher production costs; an excessive concentration does not produce any further improvements.
Treatment with lysozyme is done at a pH value in the range of 5.5 to 8.0, preferably between 6.5 and 7.5, a concentration of 0.5 to 100 ppm, and a temperature of 25° to 45° C. and even up to 60° C. for at least 20 minutes. A temperature above 60° C. is undesirable because it can lower the activity of lysozyme in some cases. At a pH above 8, lysozyme would not be active and, below 5.5 the physical properties of the product could deteriorate. If the concentration is less than 0.5 ppm prolonged treatment would become necessary, and even if treatment time is prolonged it may not lead to any meaningful effects. A concentration of more than 100 ppm is not warranted from an economical standpoint. Any of the two enzymatic treatment steps may precede the other.
Enzymes useful for the reduction of the invention to practice are: an alkaline protease produced by a bacterium in the genus Bacillus, such as, B. subtilis, and a lysozyme known as endo-β-1,4-N-acetylhexosaminidase which hydrolyzes the β-1,4 bonds of N-acetylglucosamine and N-acetylmuramic acid in bacterial cell walls. Generally, alkaline proteases produced by B. licheniformis, B. amylaliquifaciens, and B. pumilis are known besides that which originates from B. subtilis. As for lysozymes, there are known animal lysozymes, such as, egg white lysozymes of chickens, ducks, quails, turkeys, and geese, spleen lysozymes of dogs and rats, and lysozymes present in human urine (of leukemia patients), human milk, and tears. Plant lysozymes have been found in turnips, cabbages, and papaya juice. For the present invention, however, the origins of the enzymes are of little importance.
The process according to the invention permits the omission of such complex process steps as dilution, cake filtration, and concentration that have hitherto been required for the removal of undissolved matter. This brings ease of operation and economical advantage. A further advantage is high transparency of the product that ordinary enzymatic processes have failed to realize.
An important aspect of the present invention is our discovery that when specific hyperproducing X. campestris are used to generate the xanthan gum, the clarification process of the present invention yields a xanthan gum product exhibiting substantially improved transparency compared to the parent X. campestris strain from which they are derived. Strain X59 which is a rifampicin resistant strain and strain X50 which is a rifampicin and bacitracin resistant strain of X. campestris are considered hyperproducers to the extent that the strains exhibit enhanced productivity of xanthan gum as compared to strain X55 from which the hyperproducing strains are derived by a selection process as described in U.S. Pat. 5,194,386 and application Ser. No. 07/826,095. Accordingly, we have discovered a method for producing a xanthan gum broth and xanthan gum product exhibiting improved clarity as evidenced by its transparency in a 1% aqueous solution by subjecting strains X59 or X50 to submerged fermentation conditions to produce a broth of xanthan gum product. The broth thus obtained is subjected to a heat treatment as described hereinabove. Thereafter, the heat treated broth is then subjected to sequential enzymatic treatment with a protease enzyme and a lysozyme enzyme in accordance with the procedures described hereinabove. The resulting xanthan gum product may then be recovered from the broth in a conventional manner.
It should be understood, as described herein, that the inventive clarification process may be carried out on the fermentation broth, i.e., the broth after completion of the fermentation process, or, alternatively, on recovered xanthan product (i.e., in water).
The following Examples illustrates the invention.
______________________________________
I. Preproduction medium
II. Production medium
______________________________________
Glucose 5.8 g/l Glucose 58 g/l
Polypeptone 5.2 " Polypeptone
2 "
Yeast extract
2.6 " KH.sub.2 PO.sub.4
2 "
NaCl 9 " MgSO.sub.4.7H.sub.2 O
0.5 "
Water 1.8 l Water 16.2 l
______________________________________
A medium of composition II was placed in a 30-liter fermenter and inoculated with a Xanthomonas campestris broth of X59 that had been cultured for 24 hours on a medium of composition I. It was then cultured under aeration and agitation at pH 6.5 to 7.0 and at 30° C. for two days, and a broth containing 30 g xanthan gum per liter was obtained. With stirring the broth was heat-treated at an initial pH of 11° and at 55° C. for 90 minutes and, while being kept at 55° C. the broth was adjusted to pH 8.5 and, after the addition of 300 ppm alkaline protease ("Bioplase", a product of Nagase Biochemical Co.), the mixture was treated with stirring at 55° C. for two hours. Next, the resulting broth was cooled down to 35° C., 3 ppm lysozyme ("Lysozyme Taiyo", a product of Taiyo Chemical Co.) was added, and the mixture was further treated with stirring at 35° C. for one hour.
A broth prepared in the same way as described in Example 1 was enzymatically treated in the reverse order. After cooling, it was adjusted to pH 7.0 and, with the addition of 3 ppm lysozyme ("Lysozyme Taiyo" of Taiyo Chemical), the mixture was treated with stirring at 35° C. for two hours. Next, the broth was heated to 55° C., 300 ppm alkaline protease ("Bioplase" of Nagase Biochemical) was added, and the mixture was treated with stirring at 55° C. for one hour.
For the purposes of analysis, the broth was sampled after each of the process steps, i.e., after the conclusion of fermentation, the heat treatment, and the first and second stages of enzymatic treatment. Xanthan gum was separated by extraction from the test broth using 1.6 times by weight of isopropyl alcohol, and the extract was air dried. An aqueous solution containing 0.3 percent by weight of the thus obtained solid xanthan gum was prepared, and the sample was tested for light transmittance and viscosity (with a Brookfield viscometer at 30 rpm). Table 1 summarizes the results.
TABLE 1
______________________________________
Example 1
Trans- Example 2
Process Step
mittance Viscosity
Transmittance
Viscosity
______________________________________
after 11% 290 cp 12% 300 cp
fermentation
after heat
18% 290 cp 20% 290 cp
treatment
1st stage 65% 300 cp 62% 300 cp
enzymatic
treatment
2nd stage 94% 305 cp 94% 300 cp
enzymatic
treatment
______________________________________
The procedure of Example 1 was repeated for treatments except that the lysozyme concentration was varied. The results are given in Table 2.
TABLE 2
______________________________________
Example 3
Lysozyme 30 ppm
Example 4
Trans- Lysozyme 1 ppm
Process Step
mittance Viscosity
Transmittance
Viscosity
______________________________________
after 11% 280 cp 12% 300 cp
fermentation
after heat
18% 290 cp 20% 295 cp
treatment
1st stage 65% 290 cp 65% 310 cp
enzymatic
treatment
2nd stage 97% 290 cp 90% 300 cp
enzymatic
treatment
______________________________________
Fermentation performed in the same manner as in Example 1 yielded a broth containing 30 g xanthan gum per liter. With stirring, the broth at an initial pH of 7.0 was heat treated at 80° C. for 90 minutes and then cooled to and kept at 55° C. After the cooling the pH was adjusted to 8.5, and 300 ppm alkaline protease ("Bioplase" of Nagase Biochemical) was added, and the mixture was treated with stirring at 55° C. for two hours. Next, the broth was cooled down to 35° C. and after the addition of 3 ppm lysozyme ("Lysozyme Taiyo" of Taiyo Chemical), the mixture was treated with stirring at 35° C. for one hour.
For analysis, the broth was sampled after each of the process steps, i.e., after the conclusion of fermentation, the heat treatment, and the first and second stages of enzymatic treatment. Xanthan gum was separated by extraction from the test broth using 1.6 times by weight of isopropyl alcohol, and the extract was air dried. An aqueous solution containing 0.3 percent by weight of the thus obtained solid xanthan gum was prepared, and the sample was tested for light transmittance and viscosity (with a Brookfield viscometer at 30 rpm). Table 3 shows the results.
TABLE 3
______________________________________
Example 5
Process Step Transmittance
Viscosity
______________________________________
after fermentation
11% 290 cp
after heat treatment
8% 275 cp
1st stage enzymatic
46% 300 cp
treatment
2nd stage enzymatic
90% 305 cp
treatment
______________________________________
As shown in the above Examples, the invention procedure enables the production of xanthan gum having excellent viscosity, e.g., at least greater than about 175 cp (0.3% by weight solution with Brookfield viscometer at 30 rpm).
Fermentation and heat treatment were carried out in a manner similar to Example 1, and either lysozyme or alkaline protease alone was used in enzymatic treatment. The conditions for treatment with either enzyme were the same as used in Example 1. After each test period xanthan gum was separated from the resulting broth by extraction with 1.6 times by weight of isopropyl alcohol and the extract was air dried. An aqueous solution containing 0.3 percent by weight of the xanthan gum so obtained was prepared and tested for light transmittance and viscosity. As Table 4 indicates, the solutions thus prepared failed to attain, despite extended treating periods, the high transparency that the process of the present invention achieves.
TABLE 4
______________________________________
Comparative Example 1
Comparative Example 2
Treating
Lysozyme 30 ppm Alkaline Protease
Time Transmittance
Viscosity
Transmittance
Viscosity
______________________________________
untreated
35% 290 cp 35% 290 cp
2 hours
60% 300 cp 62% 300 cp
4 hours
62% 300 cp 65% 300 cp
6 hours
64% 300 cp 69% 300 cp
______________________________________
In the manner described in Example 1, fermentation and heat treatment were performed, with the exception that the enzymatic treatment used lysozyme and alkaline protease together. The reaction conditions were pH 7.5 and 45° C. at which both enzymes were active. With the addition of 300 ppm Bioplase and 3 ppm lysozyme, the reaction was carried out for 6 hours. After each treating time the sample was tested for light transmittance and viscosity as was the case with Comparative Example 1. The results are given in Table 5.
TABLE 5
______________________________________
Comparative Example 3
Treating time Transmittance
Viscosity
______________________________________
untreated 35% 290 cp
2 hours 63% 310 cp
4 hours 65% 310 cp
6 hours 69% 310 cp
______________________________________
The fermentation of Example 1 was directly by the two stage enzymatic treatment without the heat treatment. Samples of the individual process steps were tested for light transmittance and viscosity. Table 6, which shows the results, indicates that the omission of heat treatment reduced the enzymatic effects of the resulting broths.
TABLE 6
______________________________________
Comparative Example 4
Process step Transmittance
Viscosity
______________________________________
after fermentation
11% 300 cp
1st stage enzymatic treatment
40% 310 cp
2nd stage enzymatic treatment
60% 310 cp
______________________________________
A series of experiments was carried out wherein xanthan gum was produced by the submerged fermentation of strains X59 and X50. The fermentation procedures were carried out using conventional aerobic submerged fermentation techniques normally used for fermentation of X. campestris. The fermenter size was a 5 liter jar for these experiments.
The broths from each of the terminated fermentations were adjusted to pH 11 and then heated at 55° C. for 90 minutes. Thereafter, a series of four 200 ml aliquots from each of the resulting broths were treated as follows:
Each of the four aliquots were treated with a different system of protease and lysozyme enzymes. For this purpose the pH of the aliquot was adjusted to an appropriate pH for the particular protease. Table 7 sets forth a series of proteases commercially available and their optimum pHs and temperatures of use. Also shown is a Food Grade Lysozyme which was used in addition to the Lysozyme Taiyo used in the previous experiments.
TABLE 7
__________________________________________________________________________
Optimum
Optimum
Enzyme
Goods Origin
Maker Form pH Temp. °C.
__________________________________________________________________________
Protease
1.
PTN Trypsin
Novo powder
7-8 40-60
2.
Neutrase
Bacillus
Novo powder
5.5-7.5
45-55
3.
Protamex
Bacillus
Novo powder
5.5-7.5
40-60
4.
Flavour-
Asper-
Novo powder
5-7 45-50
zyme gillus
5.
Multifect
Bacillus
Genencor
liquid
6-11
50-60
P-64
6.
Multifect
Bacillus
Genencor
liquid
7-10
20-65
P-3000
Lysozyme
1.
Lysozyme
egg Canadian
powder
6-7 30-60
(Food white
lysozyme
Grade)
__________________________________________________________________________
The details of the fermentation, the final amount of xanthan gum obtained, the final cellular and the ratio of cellular debris to xanthan gum are shown in Table 8. In addition, the optical density of a 1 to 7 dilution of the initial broth, the solution obtained after the heat treatment, the solution obtained after the protease treatment, and the solution obtained after the lysozyme treatment, as well as the transmittance of a 1 wt. % solution of precipitated xanthan product obtained after the heat and enzyme treatments are shown in Table 9. The particular enzymes, temperatures and pH of the treatments used are detailed after Table 9.
TABLE 8
______________________________________
EFFECT OF CLARIFICATION FOR X59
Strain X59 Batch No. 555
Jar Size 5 l
______________________________________
FERMENTATION
Final XG Final Cell
Residual Glu.
Time [Hr.]
[g/l] [g/l] [g/l] Cell/XG [-]
______________________________________
48 30.9 2.5 13.6 0.008
______________________________________
CLARIFICATION
Standard New 1 New 2 New 3
______________________________________
(1/7 OD660)
Broth 0.739 ← ← ←
Heat Treatment
0.451 ← ← ←
Protease Treatment
0.151 0.213 0.237 0.166
Lysozyme Treatment
0.075 0.044 0.034 0.038
TRANSPARENCY
1 wt. % XG 76.0 81.1 82.0 79.3
Transmittance [%]
0.3 wt. % XG 92.1 93.9 94.2 93.3
Transmittance [%]
______________________________________
TABLE 9
______________________________________
EFFECT OF CLARIFICATION FOR X55
Strain X55 Batch No. 558
Jar Size 5 l
______________________________________
FERMENTATION
Final XG Final Cell
Residual Glu.
Time [Hr.]
[g/l] [g/l] [g/l] Cell/XG [-]
______________________________________
48 21.4 2.5 18.0 0.12
______________________________________
CLARIFICATION
Standard New 1 New 2 New 3
______________________________________
(1/7 OD660)
Broth 0.791 ← ← ←
Heat Treatment
0.427 ← ← ←
Protease Treatment
0.142 0.137 0.151 0.144
Lysozyme Treatment
0.091 0.073 0.081 0.066
TRANSPARENCY
1 wt. % XG 48.6 59.9 52.9 48.9
Transmittance [%]
0.3 wt. % XG 80.5 85.7 82.6 80.7
Transmittance [%]
______________________________________
Standard New 1
Bioprose 500 ppm 55° C.
P-64 1000 ppm 55° C.
pH 8.5 Control 2 hr.
pH 8.5 Control 2 hr.
Lys.TAIYO 3 ppm 55° C.
Ca.Lys. 100 ppm 55° C.
pH 6.5 Control 1 hr.
pH 6.5 Control 2 hr.
New 2 New 3
P-64 500 ppm 55° C.
PTN 200 PPM 55° C.
pH 8.5 Control 2 hr.
pH 8.5 Control 2 hr
Ca.Lys. 30ppm 55° C.
Ca.Lys. 30 ppm 55° C.
pH 6.5 Control 1 hr.
pH 6.5 Control 2 hr.
______________________________________
For all of the experiments described herein, the transmittance was measured using a quartz cell having a cell length of 2 cm with a lightwave length of 650 nm. Measurements were made with a photoelectric colorimeter 5E-type available from Kotaki Trading. The optical density at 660 nm was measured using a cell having a cell length of 1 cm and a dilution of 7 times by weight. Measurements were made with a UV visible recording spectrophotometer UV-160 type available from Shimazu. The results of these experiments show that substantially higher clarification of broths obtained from the fermentation of X59 are obtained by the inventive treatments as compared to the broth obtained from the fermentation of X55.
In addition, these experiments show that additional enzymes, e.g., Multifect P-64 and Canadian Lysozyme perform as well as the standard enzymes Bioplase and Lysozyme Taiyo. Preferred enzymatic treatment conditions for Multifect P-64 and Canadian Lysozyme are shown in Table 10. It is noted that pH adjustments were carried out with either 10% aqueous sulfuric acid or 20% aqueous sodium hydroxide depending on whether the pH needed to be decreased or increased. In addition, the protease "Bioplase", which is a produce of Nagase Biochemical Co., is commercially obtained as a powder absorbed or disbursed on calcium carbonate. Thus, for use, the powder is mixed with water resulting in dissolution of the enzyme into the aqueous phase. The calcium carbonate is separated from the aqueous phase and it is the aqueous phase which is used. In addition, all concentrations of enzymes are indicated as the concentration in the solution to which they are added, e.g., 500 ppm of enzymes means that in the aliquot or broth, the concentration of enzyme in solution for the treatment was 500 ppm.
TABLE 10
______________________________________
ENZYMATIC TREATMENT CONDITION
______________________________________
Protease Lysozyme
______________________________________
Goods Multifect P-64
Food Grade Lysozyme
Condition (Genencor) (Canadian Lysozyme)
Addition 500 ppm 30 ppm
pH pH 8.5 Control
pH 6.5 Control
Temp. 55° C.
55° C.
Time 2 hr. 1 hr.
______________________________________
A series of fermentations using X59, X50 and X55 were carried
out: Example 8
Media 1
Seed Media Production Media
______________________________________
Glucose 5.8 g/l Glucose 58 g/l
Polypeptone
5.2 g/l Polypeptone 2.0 g/l
Yeast extract
2.6 g/l KH.sub.2 PO.sub.4
2.0 g/l
NaCl 9.0 g/l MgSO.sub.4.7H.sub.2 O
0.5 g/l
Water 1.8 l Water 16.2 l
______________________________________
Strain X55 was used. A production media was placed in a 30 liter fermenter and inoculated with a Xanthornonas campestris broth that had been cultured for 24 hours in seed media. It was then cultured under aeration and agitation at pH 6.5 to 7.0 and at 30° C. for two days, and a broth containing 20 g xanthan gum per liter was obtained. The broth was heat-treated with stirring at an initial pH of 11 and at 55° C. for 90 minutes and while being kept at 55° C., the broth was adjusted to pH 8.5 with 10% aqueous H2 SO4. After the addition of supernatant of an aqueous solution of 9.0 g (500 ppm) alkaline protease; "Bioplase" a product of Nagase Biochemical Co., the mixture was heated with stirring at 55° C. for two hours. Next, the pH was adjusted to 6.5 and an aqueous solution of 0.054 g (3 ppm) lysozyme "Lysozyme Taiyo", a product of Taiyo Chemical Co., was added. The mixture was heated with stirring at 55° C. for one hour.
The procedure of Example 1 was repeated except that protease Multifect P-64, a product of Genencor, was used in place of Bioplase and lysozyme "Canadian Lysozyme", a product of Food Grade Lysozyme, was used in place of Lysozyme Taiyo.
The procedure of Example 1 was repeated except that strain X59 was used in place of X55.
The procedure of Example 1 was repeated except that strain X59 was used in place of X55, protease "Multifect P-64" was used in place of Bioplase and lysozyme "Canadian Lysozyme" was used in place of Lysozyme Taiyo.
The procedure of Example 1 was repeated except that strain X50 was used in place of X55.
The procedure of Example 1 was repeated except that strain X59 was used in place of X55 and Media 2 was used in place of Media 1.
______________________________________
Media 2
Seed Media Production Media
______________________________________
Glucose 5.8 g/l Glucose 58 g/l
Polypeptone
5.2 g/l NH.sub.4 NO.sub.3
1.7 g/l
Yeast extract
2.6 g/l KH.sub.2 PO.sub.4
2.0 g/l
NaCl 9.0 g/l MgSO.sub.4.7H.sub.2 O
0.5 g/l
Water 1.8 l Water 16.2 l
______________________________________
The procedure of Example 1 was repeated except that strain X50 was used in place of X55 and that Media 2 was used in place of Media 1.
A broth was prepared used in strain X59 in place of X55 in the same way as described in Example 1. The resulting broth was enzymatically treated in the reverse order, that is, after heat-treatment, it was adjusted to pH 6.5 and, after the addition of aqueous solution of 0.054 g (3 ppm) lysozyme, "Lysozyme Taiyo", the mixture was heated with stirring at 55° C. for one hour. Next, a supernatant of aqueous solution of 9.0 g (500 ppm) alkaline protease "Bioplase" was added and the mixture was heated with stirring at 55° C. for two hours.
The enzyme treatments used in the above experiments are characterized hereafter as Method A and Method B.
Heat treatment: initial pH 11, 90 minutes
Protease treatment: 500 ppm, pH 8.5, 55° C., 120 minutes ("Bioplase", a product of Nagase Biochemical Co.)
Lysozyme Treatment: 3 ppm, pH 6.5, 55° C., 60 minutes ("Lysozyme Taiyo", a product of Taiyo Chemical Co.)
Heat Treatment: initial pH 11, 90 minutes
Protease treatment: 550 ppm, pH 8.5, 55° C., 120 minutes ("Multifect P-64", a product of Genencor)
Lysozyme treatment: 30 ppm, pH 6.5, 55° C., 60 minutes ("Canadian Lysozyme", a product of Food Grade Lysozyme).
As shown in Table 11, broths and xanthan gum produced from strains X59 and X50 exhibit substantially superior transmittance using the inventive procedure as compared to the original strain X55.
TABLE 11
__________________________________________________________________________
Strain X55 X55 X59 X59 X50
Example 8 9 10 11 12
Media media1
media1
media1
media1 media1
Fermentation Result
Time [Hr] 48 48 48 48 48
Final XG [g/L]
21.4
22.1 29.5
30.9 28.8
Final Cell [g/L]
2.5 2.6 1.9 2.5 2.2
Residual Glu. [g/L]
18.0
18.4 10.5
13.6 5.6
OD660 of diluted broth
Enzyme treatment
A B A B A
Broth 0.791
0.883 0.658
0.739 0.912
Heat treatment
0.427
0.455 0.315
0.451 0.334
Protease treatment
0.142
0.136 0.100
0.237 0.098
Lysozyme treatment
0.091
0.072 0.046
0.034 0.028
Transmittance [%]
1% XG aqueous solution
48.6
58.9 87.1
82.0 85.9
0.3% XG aqueous solution
80.5
85.3 95.9
94.2 95.5
Strain X59 X50 Strain X59
Example 13 14 Example 15
Media media2
media2
Media media1
Fermentation Result Fermentation Result
Time [Hr] 48 48 Time [Hr] 48
Final XG [g/L]
34.6
29.4
Final XG [g/L]
28.6
Final Cell [g/L]
2.1 3.4 Final Cell [g/L]
2.1
Residual Glu. [g/L]
0.8 0.0 Residual Glu. [g/L]
8.3
OD660 of diluted broth
OD660 of diluted broth
Enzyme treatment
A A Enzyme treatment
A (reverse)
Broth 0.856
1.298
Broth 0.672
Heat treatment
0.454
0.494
Heat treatment
0.344
Protease treatment
0.168
0.128
Protease treatment
0.226
Lysozyme treatment
0.068
0.037
Lysozyme treatment
0.032
Transmittance [%] Transmittance [%]
1% XG aqueous solution
80.9
83.3
1% XG aqueous solution
83.3
0.3% XG aqueous solution
93.8
94.7
0.3% XG aqueous solution
94.7
__________________________________________________________________________
Claims (8)
1. A process for the preparation of purified xanthan gum, comprising:
a) subjecting strain ATCC 55429 or ATCC 55298 to submerged fermentation conditions to produce a fermentation broth containing xanthan gum and cellular debris;
b) heating the fermentation broth obtained from step a) at a temperature from 45° to 80° C. for a period of at least 30 minutes at an initial pH of 7 to 12.5;
c) contacting the heated broth from step b) with an alkaline protease for a period of from 20 minutes to five hours;
d) contacting the broth from step b) with lysozyme for a period of from 20 minutes to five hours; and
e) recovering the xanthan gum from the broth from step d).
2. A process for the preparation of xanthan gum having high transmittance in aqueous solution, comprising:
a) subjecting strain ATCC 55429 or ATCC 55298 to submerged fermentation conditions to produce a fermentation broth containing xanthan gum and cellular debris;
b) heating the fermentation broth obtained from step a) at a temperature from 45° to 80° C. for a period of at least 30 minutes at an initial pH of 7 to 12.5;
c) contacting the heated broth from step b) with lysozyme for a period of from 20 minutes to five hours;
d) contacting the broth from step c) with an alkaline protease for a period of from 20 minutes to five hours; and
e) recovering the xanthan gum from the broth from step d).
3. The process of claim 1 or 2 wherein the temperature of the heating step is from 45° C. to 70° C. and the initial pH is from 9 to 12.5.
4. The process of claim 1 or 2 wherein the contacting with alkaline protease is carried out by the addition of 10 to 500 ppm of alkaline protease to the fermented broth at a temperature of 40° to 65° C. and a pH of 6.0 to 10.0 for at least 30 minutes.
5. The process of claim 1 or 2 wherein the contacting with the lysozyme is carried out by the addition of 0.5 to 100 ppm of the lysozyme to the fermented broth at a temperature of 25° to 45° C. and a pH of 5.5 to 8.0 for at least 30 minutes.
6. The process of claim 1 or 2 wherein the xanthan gum recovered has a transmittance of at least 75% in 1% by weight aqueous solution.
7. The process of claim 1 or 2 wherein the xanthan gum recovered has a transmittance of at least 80% in 1% by weight aqueous solution.
8. The process of claim 1 or 2 wherein the xanthan gum recovered has a transmittance of at least 90% in 0.3% by weight aqueous solution.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/345,076 US5595892A (en) | 1991-12-20 | 1994-11-28 | Process for preparation of purified xanthan gum |
| US08/484,566 US5679556A (en) | 1992-12-15 | 1995-06-07 | Process for the recovery and purification of xanthan gum |
| US08/484,477 US5702927A (en) | 1991-12-20 | 1995-06-07 | Process for preparation of purified xanthan gum |
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3-338244 | 1991-12-20 | ||
| JP33824491 | 1991-12-20 | ||
| JP4054898A JP2759394B2 (en) | 1991-12-20 | 1992-03-13 | Method for producing purified xanthan gum |
| JP4-054898 | 1992-03-13 | ||
| US07/990,758 US5705368A (en) | 1991-12-20 | 1992-12-15 | Process for preparation of purified xanthan gum |
| US08/345,076 US5595892A (en) | 1991-12-20 | 1994-11-28 | Process for preparation of purified xanthan gum |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/990,758 Continuation-In-Part US5705368A (en) | 1991-12-20 | 1992-12-15 | Process for preparation of purified xanthan gum |
Related Child Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/484,477 Division US5702927A (en) | 1991-12-20 | 1995-06-07 | Process for preparation of purified xanthan gum |
| US08/484,566 Continuation-In-Part US5679556A (en) | 1992-12-15 | 1995-06-07 | Process for the recovery and purification of xanthan gum |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US5595892A true US5595892A (en) | 1997-01-21 |
Family
ID=46250137
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/345,076 Expired - Lifetime US5595892A (en) | 1991-12-20 | 1994-11-28 | Process for preparation of purified xanthan gum |
| US08/484,477 Expired - Lifetime US5702927A (en) | 1991-12-20 | 1995-06-07 | Process for preparation of purified xanthan gum |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/484,477 Expired - Lifetime US5702927A (en) | 1991-12-20 | 1995-06-07 | Process for preparation of purified xanthan gum |
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|---|---|
| US (2) | US5595892A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5994107A (en) * | 1991-12-20 | 1999-11-30 | Shin-Etsu Chemical Co., Ltd. | Process of purifying xanthan gum using an alkaline protease and lysozyme |
| US6586213B2 (en) | 2000-04-14 | 2003-07-01 | Cp Kelco U.S., Inc. | Process for clarification of xanthan solutions and xanthan gum produced thereby |
| US6709845B1 (en) | 1999-07-02 | 2004-03-23 | Shin-Etsu Bio, Inc. | Production of modified polysaccharide S-7 |
| US20060121578A1 (en) * | 2000-03-02 | 2006-06-08 | C.P. Kelco U.S., Inc. | Mutant bacterial strains of the genus sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| CN102260354A (en) * | 2010-05-28 | 2011-11-30 | 淄博中轩生化有限公司 | Preprocessing method for increasing viscosity of xanthan gum product |
| WO2018031333A1 (en) | 2016-08-10 | 2018-02-15 | Geo Fossil Fuels, Llc | Compositions comprising and methods of making bio-polymers |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6953574B2 (en) * | 2002-06-21 | 2005-10-11 | Technology Commercialization, Inc. | Method for producing a fermented hydrolyzed medium containing microorganisms |
| CA2658498C (en) * | 2005-07-22 | 2016-04-12 | Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Agriculture And Agri-Food Canada | Process for producing polysaccharide gum |
| CN107090445A (en) | 2011-11-25 | 2017-08-25 | 诺维信公司 | The polynucleotides of polypeptide and coding said polypeptide with lysozyme activity |
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Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5994107A (en) * | 1991-12-20 | 1999-11-30 | Shin-Etsu Chemical Co., Ltd. | Process of purifying xanthan gum using an alkaline protease and lysozyme |
| US6709845B1 (en) | 1999-07-02 | 2004-03-23 | Shin-Etsu Bio, Inc. | Production of modified polysaccharide S-7 |
| US7887866B2 (en) | 2000-03-02 | 2011-02-15 | Cp Kelco U.S., Inc. | Clarification of sphingans and compositions thereof |
| US20060121578A1 (en) * | 2000-03-02 | 2006-06-08 | C.P. Kelco U.S., Inc. | Mutant bacterial strains of the genus sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| US7829697B2 (en) | 2000-03-02 | 2010-11-09 | Cp Kelco Us, Inc. | Mutant bacterial strains of the genus Sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| US20110009611A1 (en) * | 2000-03-02 | 2011-01-13 | Stan Bower | Clarification of sphingans and compositions thereof |
| US8198064B2 (en) | 2000-03-02 | 2012-06-12 | Cp Kelco U.S., Inc. | Mutant bacterial strains of the genus sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| US8652792B1 (en) | 2000-03-02 | 2014-02-18 | C.P. Kelco U.S., Inc. | Mutant bacterial strains of the genus Sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| US8865241B1 (en) | 2000-03-02 | 2014-10-21 | Cp Kelco U.S., Inc. | Mutant bacterial strains of the genus Sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| US9290783B2 (en) | 2000-03-02 | 2016-03-22 | Cp Kelco U.S., Inc. | Mutant bacterial strains of the genus Sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of Sphingans and compositions thereof |
| US9725523B2 (en) | 2000-03-02 | 2017-08-08 | Cp Kelco U.S., Inc. | Mutant bacterial strains of the genus sphingomonas deficient in production of polyhydroxybutyrate and a process of clarification of sphingans and compositions thereof |
| US6586213B2 (en) | 2000-04-14 | 2003-07-01 | Cp Kelco U.S., Inc. | Process for clarification of xanthan solutions and xanthan gum produced thereby |
| CN102260354A (en) * | 2010-05-28 | 2011-11-30 | 淄博中轩生化有限公司 | Preprocessing method for increasing viscosity of xanthan gum product |
| WO2018031333A1 (en) | 2016-08-10 | 2018-02-15 | Geo Fossil Fuels, Llc | Compositions comprising and methods of making bio-polymers |
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|---|---|
| US5702927A (en) | 1997-12-30 |
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